Aqueous vinyl acrylic interpolymer emulsion and use thereof in latex paints

ABSTRACT

AN AQUEOUS POLYMER EMULSION DERIVED FROM THE INTERPOLYMERIZATION OF A SHORT-CHAIN ALPHA, BETA-UNSATURATED MONO- OR POLYCARBOXYLIC ACID, ACRYLONITRILE, A SHORT-CHAIN ALPHA, BETA-UNSATURATED AMIDE, AN ALKYL ACRYLATE, AND VINYL ACETAE OR AN ALKYL METHACRYLATE, WHEN COMBINED WITH A PIGMENTARY MATERIAL PROVIDES A LATEX PAINT WHICH, WHEN APPLIED TO A SURFACE AND CURED, FORMS A COATING EXHIBITING A HIGH DEGREE OF BURNISH RESISTANCE, SCRUB RESISTANCE, EASE OF STAIN REMOVAL, AND LOW TEMPERATURE COALESCENCE.

United States Patent US. Cl. 26029.6 TA 13 Claims ABSTRACT OF THE DISCLOSURE An aqueous polymer emulsion derived from the interpolymerization of a short-chain alpha, beta-unsaturated monoor polycarboxylic acid, acrylonitrile, a short-chain alpha, beta-unsaturated amide, an alkyl acrylate, and vinyl acetate or an alkyl methacrylate, when combined with a pigmentary material provides a latex paint which, when applied to a surface and cured, forms a coating exhibiting a high degree of burnish resistance, scrub resistance, ease of stain removal, and low temperature coalescence.

This application is a continuation-in-part of the now abandoned application Ser. No. 78,255 filed on Oct. 5, 1970.

BACKGROUND OF THE INVENTION This invention relates to latex paints and to polymer emulsions suitable for use in formulating latex paints. More particularly, the invention relates to aqueous vinyl acrylic polymer emulsions suitable for use in formulating latex paints which provide coatings of a high degree of performance.

Aqueous emulsions containing various homopolymers and copolymers (e.g., homopolymers and copolymers of vinyl esters, homopolymers and copolymers of lower alkyl acrylates such as ethyl acrylate and lower alkyl methacrylates such as methyl methacrylate, and the like) have been known for many years. Such polymer emulsions are generally prepared by adding, with rapid stirring or other suitable agitation, one or more ethylenically unsaturated monomers to water which contains or to which is added, either simultaneously or subsequently, a surfactant or emulsifying agent, a polymerization catalyst or initiator, and in many cases, a protective colloid. These mixtures are then heated to polymerization temperature with suitable agitation, and held at that temperature until substantially complete polymerization of the monomer or monomers has occurred. The resulting polymer emulsions, upon cooling and filtering, can be used in many domestic and industrial applications, such as in paints or other coating compositions (e.g., paper coatings and textile treating compositions), in adhesives or binders, in caulking compositions, and the like, depending on the nature of the particular polymer, and the properties of the emulsion containing such polymer.

With regard to paints and coatings compositions in general there has been considerable progress in recent years toward developing improved aqueous polymeric coatings compositions. These so-called water-base paints or latex paints possess a number of advantages over the traditional non-aqueous or oil-base paints. For example, latex paints are essentially odorless, non-flamable, and non-irritating to the skin. As a result, they are useful not only as household paints but also in industrial applications. With the advent of new polymers, aqueous polymeric coating compositions or latices have been developed which exhibit properties equal to or even superior to those possessed by some oil-base paints. For example, coatings derived from typical latex paints exhibit good adhesion ice to surfaces to which such paints are applied and also have excellent color retention under conditions of outdoor exposure.

Among the various aqueous polymer emulsions which are known to be useful in formulating water-base paints, acrylic polymer emulsions and particularly those which contain polymers derived from a predominant amount of a lower alkyl acrylate and minor amounts of other comonomers, e.g., alkyl methacrylates, higher alkyl acrylates, acrylic acid or methacrylic acid, vinyl halides, vinylidene halides, and the like, have come into ever-increasing use.

However, despite the great strides made in recent years,

water-base paints still possess certain disadvantages which detract from their utility. In particular, such paints generally lack resistance to burnishing, poor stain-removal properties, and poor low temperature coalescence. Burnish resistance is a desirable property which is lacking in most latex paints, particularly in fiat interior wall paints. The term burnish refers to the glossy area remaining on a painted surface after washing or rubbing the latter with a damp cloth or brush. If the burnished area is large enough, it will be noticeable and will cause the entire painted surface to appear irregular. With respect to stain removal, the only practicable method heretofore known for achieving a desirable level in this property is to sacrifice film integrity or scrub resistance. That is to say, the stains are removed by mechanical erosion of the paint film. Hence, a latex paint with good stain removal generally exhibits poor scrub or scrub resistance. The term low temperature coalesence refers to the covering power of a latex paint at the particular temperature at which it is applied to the surface to be painted. A latex paint is said to exhibit good low temperature coalesence when the individual globules of latex polymer coalesce or merge readily upon application of the latex paint to a cold surface, i.e., at below room temperature. Surfaces treated with paints having poor lowtemperature coalesence generaly require multiple coats of paint.

Whereas latex paints are known which perform well with respect to one or possibly even two of the aforementioned properties, no paint has heretofore been found which performs well in all four categories.

Therefore, it is an object of the present invention to provide aqueous polymer emulsions which serve as paint vehicles from which latex paints can be formulated having good burnish resistance, and low-temperature coalescence.

Another object is to provide a process for producing aqueous polymer emulsions which serve as paint vehicles from which latex paints can be formulated having good burnish resistance, stain removal, scrub resistance, and low temperature coalescence.

Another object is to provide a latex paint having good burnish resistance, stain removal, scrub resistance, and low temperature coalesence.

Another object is to provide a process for producing a latex paint having good burnish resistance, stain removal, scrub resistance and low temperature coalesence within the context of acrylic polymer technology.

Yet another object is to provide a wall or surface coat-ing from an acrylic latex paint having good burnish resistance, stain removal, scrub resistance, and low tem perature coalesence.

These and other objects of the invention as well as the advantages thereof can be had by reference to the following detailed description and claims.

DESCRIPTION OF THE INVENTION The above objects are achieved according to the invention by an aqueous polymer emulsion derived from the interpolymerization of a short-chain alpha,beta-unsaturated monoor polycarboxylic acid, acrylonitrile, a shortchain alpha, beta-unsaturated amide, an alkyl acrylate, and vinyl acetate or an alkyl methacrylate.

Desirably, and more particularly, the aqueous polymer emulsion paint vehicle of the present invention is a pentapolymer emulsion derived from the interpolymerization of:

(a) A short-chain alpha,beta-unsaturated monoor polycarboxylic acid, i.e., an alpha, beta-unsaturated carboxylic acid having the following formula:

wherein R is a hydrogen substituent, methyl substituent, or car-boxymethyl substituent and R and R are each independently a hydrogen substituent or a carboxyl substituent, said carboxylic acid being further characterized in that R and R are not both carboxyl substituents;

(b) Acrylonitrile;

(c) A short-chain alpha,beta-unsaturated amide, i.e., an alpha,beta-unsaturated amide having the following formula:

wherein R is a hydrogen substituent or methyl substituent and R is a hydroxymethyl substituent, an alkoxyrnethyl substituent wherein the alkyl moiety of said alkoxymethyl substituent contains between 1 and about 8 carbon atoms, or a substituent having the following structure:

wherein R is a hydrogen substituent or a hydroxymethyl substituent, with at least one of the R substituents being a hydroxymethyl substituent:

(d) An alkyl acrylate wherein the alkyl substituent contains between 1 and about 8 carbon atoms; and

(e) Vinyl acetate or an alkyl methacrylate wherein the alkyl subst'ituent contains between 1 and about 8 carbon atoms.

It is undesstood that the term pentapolymer as used herein denotes a polymer containing at least one moiety corresponding to each of the aforementioned five categories of monomer components (a) through (e). The pentapolymers of the present invention can also include those derived from more than five monomers, as when a plurality of monomers from any one or more of the categories (a), (c), (d), or (e) are employed.

Examples of alpha,beta-unsaturated monoor polycarboxylic acids suitable for use in the present invention, i.e., component (a) of the pentapolymer, include and the like. The amount or proportion of alpha-betaunsaturated monoor polycarboxylic acid employed in the present invention (including a single such acid or a plurality thereof) is ditably between about 0.25 percen by weight and about 5 percent by weight based on the total weight of the monomer components used to form the tetrapolymer. Preferably, the amount of such acid or acids ranges between about 0.3 percent by weight and about 3 percent by weight, with between about 0.4 percent by weight and about 1 percent by weight of alpha, beta-unsaturated monoor polycarboxylic acid or acids being especially preferred.

The amount or proportion of acrylonitrile used as component (b) of the pentapolymer must be greater than 5 percent by Weight and less than about 30 percent by weight based on the total weight of the monomer components used to form the tetrapolymer. Preferably, the amount of acrylonitrile ranges between about 10 percent by weight and about 20 percent by weight, with between about 10 percent by weight and about 12 percent of acrylonitrile being especially preferred.

Examples of alpha, beta-unsaturated amides suitable for use in the present invention, i.e., component (c) of the pentapolymer, include and the like. Another example of an alpha, beta-unsaturated amide suitable for use in the present invention is the class of hydroxymethyl derivative of diacetone acrylamide 4= 5= 3)2 s)2 6)3) which is commercially available from The Lubrizol Corporation under the trademark HMDAA. The 7 amount or proportion of alpha, beta-unsaturated amide employed in the present invention (including a single such amide or a plurality thereof) is desirably between about 0.5 percent by weight and about 3 percent by Weight based on the total weight of the monomer components used to form the pentapolymer. Preferably, the amount of alpha, beta-unsaturated amide or amides used ranges between about 1 percent by weight and about 2 percent by weight, with between about 1.25 percent, by weight and about 1.75 percent by weight of alpha, beta-unsaturated amide being especially preferred.

Examples of alkyl acrylates suitable for use in the present invention, i.e., component ((1) of the pentapolymer, include methyl acrylate, ethyl acrylate, n-butyl acrylate, Z-ethylhexyl acrylate, and the like. The amount of alkyl acrylate used (including a single alkyl acrylate or a plurality thereof) ranges from about 20 to about 70 percent by weight based on the total weight of the monomer components used to form the pentapolymer. Preferably, the amount of alkyl acrylate or acrylates ranges between about 30 a d about 65 per ent by Weight with be tween about 40 and about 60 percent by weight of alkyl acrylate being especially preferred.

Examples of alkyl methacrylates suitable for use in the present invention, i.e. component (e) of the pentapolymer, include methylmethacrylate, ethyl methacrylate, nbutyl methacrylate, 2-ethylhexylmethacrylate, and the like. The total amount of monomer constituting component (e), i.e., vinyl acetate and/or alkyl methacrylate, ranges from about to about 70 percent by weight based on the total weight of the monomer components used to form the pentapolymer. Preferably the amount of component (e) ranges between about and about 60 percent by weight with between about and about 50 percent by weight of component (e) being especially preferred.

The aqueous pentapolymer emulsions or latices of the present invention are prepared in an aqueous menstruum under emulsion polymerization conditions. Any of a number of procedures heretofore known for effecting such emulsion polymerizations can be employed. It is a desideratum of the present invention, however, that the mode of polymerization be such as to result in latices having viscosities consistent with the use thereof in coatings applications. Accordingly, polymerization techniques designed to elevate the viscosity of the finished latex (e.g., so-called overpolymerization of one or more viscosityeuhancing monomers over a base polymer) are outside the scope of the present invention. Desirably, the procedure used involves the addition of one or more and preferably all, of the monomeric components to the reaction sphere in emulsified form. The reaction sphere to which the monomer pre-emulsion is added can contain a polymerization catalyst, one or more dispersing agents or emulsifying agents (hereinafter collectively referred to as surfactants), and the balance, if any, of the monomer charge, preferably also in emulsified form. Optionally, the reaction sphere can contain one or more protective colloids, substances which serve to stablize the finished aqueous polymer emulsion against undesirable grit formation, coagulation, settling, and the like.

The polymerization temperature required to produce the aqueous paint vehicle of this invention will generally range from about room temperature or lower to about 100 C. or above. Preferably, the temperature employed will be between about 50 C. and about 70 C. and can, if desired, be maintained constant or varied within the aforementioned limits as the polymerization reaction proceeds toward completeion. Subatmospheric pressures, atmospheric pressure or superatmospheric pressures can be employed during all or part of the polymerization process and, depending on the monomers and other ingredients employed in the reaction, can be carried out, if desired, under a conventional inert atmosphere.

The surfactants which can be used in the preparation of the instant paint vehicles include any anionic or non-ionic surfactant or plurality or combination thereof, which are employed in preparing conventional acrylic polymer emulsions. Preferably, the surfactant system is composed of a non-ionic surfactant or plurality thereof.

Among the non-ionic surfactants which can be used are polyethers, e.g., ethylene oxide and propylene oxide condensates in general, including straight-chain and branchedchain alkyl and alkylaryl polyethylene glycols and polypropylene glycol ethers and thioethers, and, more particularly, those substances known as the Igepal surfactants which is a trademark of General Aniline and Film Corporation denoting members of a homologous series of alkylphenoxypoly(ethylenoxy)ethauols, which series can be represented by the general formula:

wherein R represents an alkyl substituent and n represents the number of moles of ethylene oxide employed. These non-ionic surfactants include alkylphenoxypoly(ethyleneoxy)ethanols having alkyl substituents containing between about 4 and about 20 carbon atoms and having between about 10 and about 240 ethyleneox units, included among which are alkylphenoxypoly(ethyleneoxy)ethanols having alkyl groups containing from about 7 to about 18 carbon atoms, and having from about 10 to about ethyleneoxy units, such as the heptylphenoxy poly(ethyleneoxy) ethanols, nonylphenoxypoly ethyleneoxy) ethanols, nonylphenoxypoly(ethyleneoxy)ethanols and dodecylphenoxypoly(ethyleneoxy)ethanols. Other suitable nonionic surfactants are the Tween surfactants, which is a trademark of Atlas Powder Company denoting polyoxyalkylene derivatives of hexitol (including sorbitans, sorbides, mannitans and mannides) anhydride, and partial esters of long-chain fatty acids such as the polyoxyalkylene derivatives of sorbitan monolaurate, sorbitan monopalmitate, sorbitan monostearate, sorbitan tristearate, sorbitan mono-laurate, sorbitan trilaurate, sorbitan mono-oleate, and sorbitan trioleate. Other classes of suitable non-ionic surfactants are the Pluronic surfactants which is a trademark of Wyandotte Chemicals Corporation denoting condensates of ethylene oxide with a hydrophobic base, said base being formed by condensing propylene oxide with propylene glycol; sulfur-containing condensates, e.g., those prepared by condensing ethylene oxide with higher alkyl mercaptans, such as nonyl mercaptan, dodecyl mercaptan, or tetradecyl mercaptan, or with alkylthiophenols wherein the alkyl group contains from 6 to 15 carbon atoms; ethylene oxide derivatives of longchain carboxylic acids such as lauric acid, myristic acid, palmitic acid, or oleic acid, or mixtures of acids such as tall oil; and ethylene oxide derivatives of long-chain alcohols such as octyl alcohol, decyl alcohol, lauryl alcohol, or cetyl alcohol.

Among the anionic surfactants which can be used are the higher molecular weight sulfates and sulfonates, e.g., sodium and potassium alkyl, aryl, and alkylaryl sulfates and sulfonates such as sodium Z-ethylhexyl sulfate, potassium 2-ethylhexyl sulfate, sodium nonyl sulfate, sodium undecy'l sulfate, sodium tridecyl sulfate, sodium pentadecyl sulfate, sodium lauryl sulfate, sodium methylbenzenesulfonate, potassium methylbenzenesulfonate, potassium toluenesulfonate and sodium xylenesulfonate; higher fatty alcohols, e.g., stearyl alcohol, lauryl alcohol, and the like, which have been ethoxylated and sulfonated: dialkyl esters of alkali metal sulfosuccinic acid salts, such as sodium diamyl sulfosuccinate; and formaldehyde/ naphthalenesulfonic acid condensation products.

The total amount of surfactant employed in the emul sion polymerization process of the present invention will range from about 1 percent by weight to about 10 percent by Weight, based on the total weight of the monomer charge, and this can be the case whether a non-ionic or anionic surfactant is employed. However, it is preferred when using typical non-ionic surfactants, eg, those of the above-described alkylphenoxypoly(ethyleneoxy)ethanols, which contain from about 4 to about 240 ethyleneoxy units, or typical anionic surfactants e.g., an ethoxylated higher fatty alcohol which has also been sulfonated, to employ them in amounts ranging from about 1.5 percent by weight to about 6 percent by weight, based on the total weight of the monomer charge.

Aside from the surfactant or surfactant mixture employed, the reaction sphere can also contain small amounts of one or more protective colloids, particularly when a reflux-type polymerization procedure is employed. Included among such materials are ether linkage-containing protective colloids such as hydroxymethyl cellulose, hydroxyethyl cellulose, ethylhydroxyethyl cellulose, carboxymethyl cellulose, ethoxylated starch derivatives, and the like. However, other protective colloid-forming substances, i.e., those containing no ether linkages, can also be used either alone or in combination with the aforementioned ether linkage-containing colloids are partially and fully hydrolyzed polyvinyl alcohols, polyacrylic acid, alkali metal polyacrylates, (e.g., sodium polyacrylates) polyacrylamide, poly-(methylvinyl ether/maleic anhydride), polyvinylpyrrolidone, water-soluble starch, glue, gelatin, water-soluble alginates such as sodium alginate or potassium alginate, casein, agar, and naturaland synthetic gums, such as gum arabic and gum tra gacanth. All of these materials can be used in amounts conventionally employed in emulsion polymerization procedures, i.e., in amounts usually ranging from about 0.1 percent by weight to about 2 percent by weight, based on the total weight of the monomer charge.

The monomeric components of the latices of the present invention are polymerized by means of catalytically effective amounts of one or more conventional free radical polymerization catalysts or catalyst systems (which are also known in the art as addition polymerization catalysts, vinyl polymerization catalysts or polymerization im tiators). Preferably, the polymerization catalyst is substantially water-soluble. Among such catalysts are inorganic peroxides such as hydrogen peroxide, alkali metal persulfates (e.g., sodium persulfate, potassium persulfate) or and alkali metal perborates, azonitriles such as ambisisobutyronitrile, and redox systems, including such combinations as mixtures of hydrogen peroxide t-butyl hydroperoxide, and the like, and any of an iron salt, a titanous salt zinc formaldehyde sulfoxylate or sodium formaldehyde sulfoxylate; alkali metal persulfate or ammonium persulfate perborate or perchlorate together with an alkali metal bisulfite such as sodium metabisulfite; and an alkali metal persulfate together with an arylphosphinic acid such as benzenephosphinic acid, and the like.

In accordance with conventional practice, the amount of polymerization catalyst employed in the present process is generally no more than that required to obtain substantially complete monomer conversion at lowest catalyst cost. Thus, for example, there can be employed from about 0.3 percent by weight to about 0.5 percent by weight of a perchlorate such as ammonium perchlorate, together with an approximately equal amount of a bisulfite such as sodium metabisulfite, and preferably about 0.4 percent by weight of the perchlorate together with about 0.4 percent by weight of the bisulfite, each of these weight percentages being based on the total weight of the monomer charge.

It is also possible, when using a redox catalyst system, to dissolve the oxidant, e.g., ammonium persulfate, in the surfactant-water mixture constituting the original reaction sphere prior to the addition of the monomer pre-emulsion. Thereafter, the reductant, together with the monomer pre-emulsion (which can likewise contain dissolved oxidant), can be added to the reaction sphere in separate aqueous streams.

The amounts of water used to form the reaction sphere, monomer pre-emulsion and catalyst solutions are generally determined by the solids content desired in the finish'ed polymer emulsion. The latex solids content can range from as low as 20 percent by weight or lower to as high as 70 percent by weight or higher, based on the total weight of the emulsion.

The pentapolymer latices as produced generally have a pH in the acid range. Although these acidic latices can be formulated into paints, better results are obtained by adjusting the pH to at least 6.8 and desirably to a pH greater than 7. For example, undesirable corrosion of metallic substrates and containers (can corrosion) can be suppressed by simply imparting an alkailne pH to the latex. Especially preferred is a latex having a pH between about 7 and about 10. Materials suitable for use in adjusting the pH to the desired value generally include any alkaline material and desirably one which does not form a strong electrolyte. Examples of suitable materials include metal hydroxides, e.g., potassium hydroxide; and amines e.g., ammonia piperidine dimethylaniline, morpholine, mono-, di-, and triethanolamine, and n-butylamine. Ammonium hydroxide (aqueous ammonia) is especially preferred for adjusting the latex pH because of its low cost and high volatility (i.e., during the Curing of the latex paint, ammonia is released from the ammonium carboxylate sites along the polymer chains).

It is 'a principal feature of the present invention that pentapolymer latices of the type described hereinabove can be used to formulate water-base paints having extraordinarily good performance properties. The formulation procedure used can be any of those heretofore known in the latex paint formulation art. Essentially, the water-base paints of the present invention comprise an admixture of pigmentary material (including primary pigments and extender pigments) and latex. The pigmentary material is preferably utilized in conventionally suitable comminuted form as are all of the other optional solid adjuvants described hereinbelow.

In combining the paint constituents to formulate a latex paint of the present invention, one or more primary pigments, extender pigments, and other adjuvants (which may themselves be liquid or solid), if any, can be incorporated into the pentapoly-mer latex binder to form a smooth, uniform mixture simply by adding all the materials to a vessel with stirring. While it is possible to combine pigments and the like with the pentapolymer emulsion and to grind or otherwise triturate the admixture in a mill, it is desirable to first prepare an aqueous paste of pigment and adjuvants, preferably With the aid of a dispersing agent, in a high-shear mixture and then combine the paste with the latex. The consistency of the paste can be controlled by the relative amounts of Water and pigments and adjuvants used.

Pigmentary material suitable for use in formulating the Water-base paints of the present invention include (but are not limited to) conventional primary pigments or color bodies such as titanium oxide, carbon black, cadmium sulfide, cadmium selenide, copper phthalocyanine, zinc oxide, zinc sulfide, iron oxide, chromium oxide, and the like. The proportion of pigmentary material used in formulating a water-base paint of the present invention is expressed herein in terms of pigment volume concentrations (PVC), according to the following relationship:

Volume of Pigmentary MaterialX Volume of Pigmentary Material +Volume of Latex Solids The choice of a particular pigment volume concentration is determined by a number of factors, including the desired depth of color, covering power, and the like. Generally, the water-base paints of. the present invention can have pigment volume concentrations ranging from about 20 percent or less up to about 75 percent. Preferably, these water-base paints have pigment volume concentrations of between about 45 percent and about 70 percent.

In addition to primary pigments, one or more various extender pigments or other adjuvants can, if desired, be included in the formulation of the water-base paints of the present invention. Such materials include (but are not limited to) dispersing and emulsifying agents; thickeners; sizing agents; fillers (i.e., extender pigments coalescing agents; antifreeze agents; filming agents; protective colloids; and the like. The selection of particular adjuvants and the relative amounts thereof are generally governed by the properties desired in a particular waterbase paint and will be apparent to those skilled in the art. In general however, the latex paints of the present invention will have total solids contents between about 40 and about 65 weight percent.

The water-base paints of the present invention can be applied to a wall surface or substrate surface in any conventional manner, e.g., by brush, roller, spraying, and the like. The paint can be cured or dried after application to the substrate, likewise by conventional means, e.g., air drying, baking, and the like. The cured paint coating exhibits excellent performance with regard to burnish resistance, scrub resistance, stain removal and low temperature coalesence. In addition, surfaces coated with the latex paints of the present invention perform well with regard to enamel holdout and contrast ratio (i.e., hiding power). These properties are further defined and illustrated in connection with the following description of the preferred embodiments.

DESCRIPTION OF PREFERRED EMBODIMENTS The following examples are presented for the purpose of illustrating (but not limiting) the present invention. In the examples:

Parts and percentages are by weight unless otherwise indicated.

Scrub resistance is determined according to a modified version of ASTM-2486-66T. The test paint is drawn down the length of a black plastic (Laneta) panel using a 7 millimeter applicator and the resulting film is allowed to dry for 7 days at 77 F. and 50 percent relative humidity. The test panel is placed on the shim plate and fastened with masking tape around the perimeter. The shim plate is then placed in the pan holder of the washability tester. An amount (5.0 grams) of Bon Ami abrasive is placed directly on the wet nylon brush (which had been immersed in distilled water overnight), and the brush mounted on the test panel with a l-pound weight attached to the top of the brush holder. The washability tester is started, and, after every 300 cycles, the brush is rewetted and an additional grams of abrasive is added thereto. Two panels are tested for each paint sample.

Readings (number of cycles) are taken at the complete break of the paint film across the width of the shim. Scrub resistance is determined by averaging the two readings (one reading for each panel).

Burnish resistance is determined by visual examination of the panels during the above-described scrub resistance test procedure.

Stain removal is determined using the films prepared in connection with the scrub resistance test, supra. The following stains are applied to the panels 0.5 hour prior to testing: Bleisdell red china marking; lead pencil (2 /2 hardness); red crayon; and house dust. The test panels are subjected to the scrub resistance test procedure and the number of cycles required to remove each stain is recorded.

Viscosity is determined by means of a Stormer viscometer equipped With a paddle-type rotor. The paint to be tested is stirred thoroughly and placed in a cylindrical container having an inside diameter of at least 3 inches. The temperature of the paint sample is maintained at 75i3 F. This is the temperature at which the results in column 3 of Table I, infra, are obtained. The results shown in columns 4 and 5 of Table I were obtained at 120 F. The paddle is rotated in the paint sample for at least 10 cycles. The time required for an additional 100 cycles is then measured. The weights selected are those which will result in a time of 27 to 33 seconds for the 100 cycles. The viscosity in Krebs Units is determined from the table accompanying the Stormer viscometer.

Enamel holdout is determined by means of the following procedure. A film of the paint to be tested is applied over the unsealed section of an all-white Morest Chart (Form HC) using a 6-inch wide Bird applicator. The resulting film thickness: 1.5-2.0 mils) is allowed to dry for 24 hours. Next, a commercially available semi-gloss composition (Dulamel, produced by Benjamin Moore & Co.) is applied over the entire length of the Morest Chart using the applicator adjusted to give a dry film thickness of approximately 1.5 mils. The films thus applied is allowed to dry for 16 to 24 hours. The degree of gloss over the test paint and over the sealed surface are measured at 60 F. using a vacuum plate to produce a flat surface. The enamel holdout rating (sealing efiiciency), in percent, is determined from the following formula:

Gloss over test paintX 100 Contrast ratio is determined by means of the following procedure. A 0.003-inch film of the paint to be tested is applied over a half white, half black Morest Chart (Form 010 P) using a Bird applicator. The resulting paint film is allowed to dry for at least 16 hours. The reflectance of the test paint film over the white and black sections of the Morest Chart is measured using a Photovolt model 610 photoelectric refiectometer equipped with a 610 Y search unit. The apparatus is allowed to warm up for at least 15 minutes and then, using the green filter, it is standardized at 0 with the instrument off and at the standardized reflectance (approximately 75) using the white enamel working standard (Catalog No. 6162). The values for contrast ratio in percent, are obtained using the following formula:

Reflectance over blackXlOO Reflectance over white Low temperature coalescence is determined as follows. The test paint, unsealed cardboard test panel, and applicator brush are conditioned in a refrigerator overnight at 40 F. Upon removal, the unsealed cardboard is immediately painted with the test paint and replaced in the refrigerator to dry for approximately 4 hours while the brush and test paint are allowed to warm up to ambient temperature. Upon completion of the 4-hour drying period'the test panel is removed from the refrigerator and allowed to warm up to ambient temperature. The test paint (now at ambient temperature) is re-applied over the test panel in the form of an X. Upon re-drying at ambient temperature, the test panel is inspected visually. In the case of paints having good low temperature coalescence, the X should be undiscernible except for the slight angular sheen difference which is common to all latex paints.

Solids contents are determined gravimetrically.

EXAMPLE I This example describes the preparation of a latex paint according to the present invention wherein the paint vehicle is a pentapolymer emulsion derived from methacrylic acid, acrylonitrile, N-methylolacrylamide, ethyl acrylate, and vinylacetate.

First, a monomer pre-emulsion is prepared from the following ingredients:

Contrast ratio Ingredient Parts Water A. l 70.0 Methacrylic acid 2.5 Acrylonitrile 30.0 -N-methylolacrylamide (60% aqueous solution) 12.5 Ethyl acrylate 301.0 Vinyl acetate 277.5 Igepal CO89=7 37.1 Igepal 00-530 13.0

Total 693.6

Ingredient Parts Monomer pre-emulsion 693.6 Sodium persulfate 1.0 Sodium metabisulfite 1.0 Water 320.0

To a reaction sphere comprising initially a moderately agitated solution of sodium persulfate (1.0 part) and sodium metabisulfite (1.0 part) in water (2000 parts) are added continuously and concurrently the monomer pre-emulsion, a catalyst solution of sodiumpersulfate (1.0 part) in water (50.0 parts), and a catalyst solution of sodium metabisulfite 1.0 part) in water (50.0 parts). The pro-emulsion is added over a period of 4- hours while the catalyst solutions are both added over a period of 4 hours 10 minutes, all three additions being commenced at the same time. A temperature of 65 C. is maintained with the reaction sphere throughout the additions. At the completion of the addition of the catalyst solutions, another solution of sodium persulfate (1.0 part) in water (10.0 parts) and another solution of sodium metabisulfite (1.0 part) in water (10.0 parts) are added to the reaction sphere continuously and concurrently over a period of 10 minutes. When these additions are complete, the reaction sphere is maintained at a temperature of 65 C. for an additional 1 hour and is then cooled to ambient temperature. The resulting latex has a solids content of 60 percent.

A water-base paint is formulated from the above-prepared latex by first mixing the following ingredients, in the order indicated, within a suitable vessel:

Ingredient Pounds Gallons 2% aqueous solution of Methocel 65 HG (a trade mark oi Dow Chemical Co. denoting a watersoluble methyl cellulose)- 165 18. 5 Potassium tripolyphosphate. 1 Propylene glycol 25 2. 9 Tamol 731 (a trademark of Itohm dz Haas Co. de-

noting a 25% aqueous solution of the sodium salt of a carboxylated polyelectrolyte) 2 0. 4 B. & R 551 (a trademark of Ross & Rowe, Inc denoting a water-dispersible lecithin) 2. 0. 2 PMA 18 (a trademark of Troy Chemical Co. do-

noting an 18 percent aqueous solution of phenyl mercuric acetate) 0. 3 Rutile (pigment grade titanium dioxide) 190 5. 4 Iceberg (a trademark of Thompson, Weinmann &

Co. denoting an aluminosilicate pigment) 100 4. 6 Snowflake White (a trademark of Thompson, Weinmann & C0. denoting a calcium carbonate whiting filler) 125 5. 5 Celite 281 (a trademark oi Johns Manville Co. de-

noting diatomaceous earth filler) 25 1. 3 Napco NDW (a trademark of Napco Chemical Co.

denoting a silicone defoaming agent) 2 0. 2 Water (added incrementally during pigment addition to maintain a heavy paste) 130 15. 6 Carbitol Acetate (a trademark of Union Carbide Corp. denoting diethylene glycol monethyl ether acetate coalescing agent) 8 0. 9

Total 767. 3 55. 5

The resulting mixture is stirred until uniform, dispersed in a Cowles Dissolver, and letdown with the following ingredients:

Ingredient Pounds Gallons Water 120 14. 4 2% aqueous solution of Methocel 65 HG 50 6. 0 Tetrapolymer emulsiom 240 24. 4

Total 390 44. 4

The resulting latex paint has the following physical properties:

The performance properties of this latex paint are summarized in Table I, hereinbelow.

EXAMPLE H The procedure employed in this example is identical to that used in Example 1, except that a hydroxymethyl derivative of diacetone acrylamide (sold by The Lubrizol Corporation under the trademark I-IMDAA) is substituted for N-methylolacrylamide. Thus, a monomer preemulsion is first prepared from the following ingredients:

Ingredient: Parts Water 70.0 Methacrylic acid 2.5 Acrylonitrile 30.0 Lubrizol HMDAA (55% aqueous solution) 13.6 Vinyl acetate 227.5 Ethyl acrylate 301.0 Igepal CO897 37.1 Igepal CO-530 13.0

Total 694.7

The performance properties of the resulting latex paint are summarized in Table I, hereinbelow.

EXAMPLE III This example illustrates a variant of the procedure employed in Examples I and II to produce a pentapolymer emulsion which is subsequently formulated into a latex paint according to the present invention.

The monomer pre-emulsion is prepared in the manner of Example I from the following ingredients:

The tetrapolymer emulsion is next prepared in the manner of Example I from the following ingredients:

Ingredient: Parts Monomer pro-emulsion 527.5 Sodium persulfate 0.8 Sodium metabisulfite 0.8

Water i 467.7

To a moderately agitated solution of 0.8 part each of sodium persulfate and sodium metabisulfite in 347.7 parts of water at 65 C. are added continuously and concurrently the monomer pre-emulsion, a catalyst solution of sodium persulfate (0.8 part) in water (50.0 parts), and a catalyst solution of sodium metabisulfite (0.8 parts) in water (50.0 parts). The rates of addition and reaction temperature are the same as in Example I. Upon' the completion of the additions, another solution of sodium persulfate (0.8 part) in water (10.0 parts) and another solution of sodium metabisulfite (0.8 part) in water (10.0 parts) are added to the reaction mixture continuously and concurrently over a period of 10 minutes at 65 C. When these additions are complete the reaction system is maintainedat a temperature of 65 C. for an additional 1 hour and then cooled to room temperature. The latex has a solids content of 46 percent.

Two water-base paints, each with a difierent pigment volume concentration (PVC), are formulated from the tetrapolymer latex produced above in this example by 13 first mixing the following ingredients, in cated within a suitable vessel:

the order indi- The resulting mixture is stirred until uniform, dispersed in a Cowles Dissolver, and let down with the following ingredients:

Ingredient Pounds Gallons Water and/or a 1.25% aqueous solution of Natrosol 250 HR (for viscosity adjustment) 267 32. Tetrapolyrner emulsion for 50 PVC 358 38. 4 60 PVC 237 25. 4

The resulting latex paints have the following physical properties:

Pigment volume concentration (PVC): 50 or 60% Density (pounds/gallon) 11.0 Solids content (weight percent) 50.2 pH 8.0-9.0 Viscosity (Krebs Units K.U.) ca 80-90 The performance properties of these latex paints are summarized in Table 1, below.

EXAMPLE IV The procedure employed in this example is identical to that used in Example III, except that Lubrizol, HMDAA is substituted for N-methylolacrylamide. Thus, the monomer pro-emulsion is first prepared in the manner of Example I from the following ingredients:

The performance properties of the resulting latex paints are summarized in Table I, below.

monomer charge of an alpha,beta-unsaturated carboxylic acid having the following formula:

wherein R is a hydrogen substituent, methyl substituent, or carboxymethyl substituent and R and R are each independently a hydrogen substituent or a carboxyl substituent, said carboxylic acid being further characterized in that R and R are not both carboxyl substituents;

(b) greater than 5 percent by weight and less than about 30 percent by weight based on the total weight of the monomer charge of acrylonitrile;

(c) between about 0.5 percent by weight and about 3 percent by weight based on the total weight of the monomer charge of an alpha, beta-unsaturated amide having the following formula:

wherein R is a hydrogen substituent or methyl substituent and R is a hydroxymethyl substituent, an alkoxymethyl substituent wherein the alkyl moiety of said alkoxymethyl substituent contains between 1 and 8 carbon atoms, or a substituent having the following structure:

CH3 Ru 0 Re (1H3 I ia Ra wherein R is a hydrogen substituent or a hydroxymethyl substituent, with at least one of the R substituents being a hydroxymethyl substituent;

(d) between about 20 percent by weight and about 70 percent by weight based on the total weight of the monomer charge of an alkyl acrylate wherein the alkyl substituent contains between 1 and about 8 carbon atoms; and

(e) between about 20 percent by weight and about 70 percent by weight based on the total weight of the monomer charge of vinyl acetate or an alkyl methacrylate wherein the alkyl substituent contains between 1 and 8 carbon atoms.

2. An aqueous pentapolymer emulsion according to claim 1 wherein:

the alpha, beta-unsaturated carboxylic acid component (a) is acrylic acid, methacrylic acid, itaconic acid, maleic acid, or fumaric acid, said carboxylic acid constituting between about 0.3 percent by weight and about 3 percent by weight of the monomer charge;

the alpha, beta-unsaturated amide component (c) is N- methylolacrylamide, N-methoxymethylacrylamide, N- methylolmethacrylamide, N methoxymethylacrylamide, or a hydroxymethyl derivative of diacetone TABLE I.LATEX PAINT EVALUATION Viscosity (K.U.)

PVC Scrub Enamel Contrast Stain removal (strokes) Low tem- China. (per- 1 week at 8 weeks at resist. holdout ratio perature Burnish ma kcent) Initial 120 F. 120 F. (cycles) (percent) (percent) coalescence resistance i ng Pencil Crayon 33:

56 84 82 79 555 72. 7 96. 3 Excellent..- Excellent 56 s4 s2 79 550 72. 7 96.5 do do-. 2 79 67 64 470 70. 6 92, 6 .do 40 12 12 28 86 72 70 95 66. 1 6. 44 15 15 23 50 80 67 640 66. 0 44 15 15 23 60 86 72 300 66. 1 45 15 12 23 I claim:

acrylamide, said amide constituting between about 1 percent by weight and about 2 percent by weight of the monomer charge;

the alkyl acrylate component (d) is methyl acrylate, ethyl acrylate, n-propyl acrylate, iso-propyl acrylate, n-butyl acrylate or 2-ethylhexyl acrylate, said alkyl 15 acrylate constituting between about 30 percent by weight and about 65 percent by weight of the monomer charge; and

the alkyl methacrylate component (e) is methyl methacrylate, ethyl methacrylate, n-butyl methacrylate, or 2-ethylhexyl methacrylate, said vinyl acetate or alkyl methacrylate component (e) constituting between about 25 percent by weight and about 60 percent by weight of the monomer charge.

3. An aqueous pentapolyrner emulsion according to claim 2 wherein:

the alpha, beta-unsaturated carboxylic acid component (a) is methacrylic acid and constitutes between about 0.4 percent by weight and about 1 percent by weight of the monomer charge;

the acrylonitrile component (b) constitutes between about 10 percent by weight and about 12 percent by weight of the monomer charge;

the alpha, beta-unsaturated amide component is N- methylolacrylamide or a hydroxymethyl derivative of diacetone acrylamide and constitutes between about 1.25 percent by weight and about 1.75 percent by Weight of the monomer charge; and

the alkyl acrylate component (d) is ethyl acrylate and constitutes between about 40 percent by weight and about 60 percent by weight of the monomer charge;

and

component (e) is vinyl acetate and constitutes between about 30 percent by weight and about 50 percent by weight of the monomer charge.

4. A process for producing an aqueous pentapolymer emulsion comprising inter-polymerizing in aqueous medium a monomer charge consisting essentially of:

(a) between about 0.25 percent by weight and about percent by weight based on the total weight of the monomer charge of an alpha,beta-unsaturated carboxylic acid having the following formula:

wherein R is a hydrogen substituent, methyl substituent, or carboxymethyl substituent and R and R are each independently a hydrogen substituent or a carbonyl substituent, said carboxylic acid being further characterized in that R and R are not both carboxyl substituents;

(b) greater than 5 percent by weight and less than about 30 percent by weight based on the total weight of the monomer charge of acrylonitrile;

(c) between about 0.5 percent by weight and about 3 percent by weight based on the total weight of the monomer charge of an alpha, beta-unsaturated amide having the following formula:

HzC=(| /NH-R5 wherein R is a hydrogen substituent or methyl substituent and R is a hydroxymethyl substituent, an alkoxymethyl substituent wherein the alkyl moiety of said alkoxymethyl substituent contains between 1 and about 8 carbon atoms, or a substituent having the following structure:

CH3 Ra Ra wherein R is a hydrogen substituent or a hydroxymethyl substituent with at least one of the R substituents being a hydroxyrnethyl substituent; (d) between about 20 percent by weight and about 70' percent by weight based on the total weight of the monomer charge of an alkyl acrylate wherein the alkyl substituent contains between 1 and about 8 carbon atoms; and

(e) between about 20 percent by weight and about 70 percent by Weight based on the total weight of the monomer charge of vinyl acetate or an alkyl methacrylate wherein the alkyl substituent contains between 1 and about 8 carbon atoms.

5. A process according to claim 4 wherein:

the alpha, beta-unsaturated carboxylic acid component (a) is acrylic acid, methacrylic acid, itaconic acid, maleic acid or fumaric acid, the carboxylic acid constituting between about 0.3 perent by weight and about 3 percent by weight of the monomer charge;

the acrylom'trile component (b) constitutes between about 10 percent by weight and about 20 percent by weight of the monomer charge;

the alpha, beta-unsaturated amide component (c) is N methylolacrylamide, N methoxymethylacrylamide, N-methylolmethacrylamide, N-methoxymethylacrylarnide, or a hydroxymethyl derivative of diacetone acrylamide, said amide constituting between about 1 percent by weight and about 2 percent by weight of the monomer charge;

the alkyl acrylate component (d) is methyl acrylate, ethyl acrylate, n-propyl acrylate, iso-propyl acrylate, n-butyl acrylate or 2-ethylheXy1 acrylate, said alkyl acrylate constitutin between about 30 percent by weight and about 65 percent by weight of the monomer charge; and

the alkyl methacrylate component (e) is methyl methacrylate, ethyl methacrylate, n-butyl methacrylate, or Z-ethylhexyl methacrylate, said vinyl acetate or alkyl methacrylate component (e) constituting between about 25 percent by weight and about 60 percent by weight of the monomer charge.

6. A process according to claim 5 wherein:

the alpha, beta-unsaturated carboxylic acid component (a) is methacrylic acid and constitutes between about 0.4 percent by weight and about 1 percent by weight of the monomer charge;

the acrylonitrile component (b) constitutes between about 10 percent by weight and about 12 percent by weight of the monomer charge;

the alpha,beta-unsaturated amide component (0) is N- methylolacrylamide or a hydroxymethyl derivative of diacetone acrylamide and constitutes between about 1.25 percent by weight and about 1.75 percent by weight of the monomer charge; and

the alkyl acrylate component ((1) is ethyl acrylate and constitutes between about 40 percent by weight and about 60 percent by weight of the monomer charge; and

component (e) is vinyl acetate and constitutes between about 30 percent by weight and about 50 percent by weight of the monomer charge.

7. A latex paint comprising a pigmentary material and an aqueous pentapolymer emulsion, said emulsion being derived from the interpolymerization of a monomer charge consisting essentially of:

(a) between about 0.25 percent by weight and about 5 percent by weight based on the total weight of the monomer charge of an alpha, beta-unsaturated carboxylic acid having the following formula:

R: C OOH (b) greater than 5 percent by weight and less than about 30 percent by weight based on the total weight of the monomer charge of acrylonitrile;

(c) between about 0.5 percent by weight and about 3 percent by Weight based on the total weight of the monomer charge of an alpha, beta-unsaturated amide having the following formula:

wherein R is a hydrogen substituent or methyl substituent and R is a hydroxymethyl substituent, an alkoxymethyl substituent wherein the alkyl moiety of said alkoxymethyl substituent contains between 1 and about 8 carbon atoms, or a substituent having the following structure:

CH: Re B J; ll 5 R 0 (EH; Iia a wherein R is a hydrogen substituent or a hydroxymethyl substituent with at least one of the R substituents being a hydroxymethyl substituent;

(d) between about 20 percent by weight and about 70 percent by weight based on the total weight of the monomer charge of an alkyl acrylate wherein the alkyl substituent contains between 1 and about 8 carbon atoms; and

(e) between about 20 percent by weight and about 70 percent by weight based on the total weight of the monomer charge of vinyl acetate or an alkyl methacrylate wherein the alkyl substituent contains between 1 and about 8 carbon atoms.

8. A latex paint according to claim 7 wherein:

the alpha, beta-unsaturated carboxylic acid component (a) is acrylic acid, methacrylic acid, itaconic acid, maleic acid or fumaric acid, said carboxylic acid constituting between about 0.3 percent by weight and about 3 percent by weight of the monomer charge;

the acrylonirtile component (b) constitutes between about percent by weight and about 20 percent by weight of the monomer charge;

the alpha,beta-unsaturated amide component (c) is N- methylolacrylamide, N methoxymethylacrylamide, N-methylolmethacrylamide, N-methoxymethylacrylamide, or a hydroxymethyl derivative of diacetone acrylamide, said amide constituting between about 1 percent by weight and about 2 percent by weight of the monomer charge;

the alkyl acrylate component (d) is methyl acrylate, ethyl acrylate, n-propyl acrylate, iso-propyl acrylate, n-butyl acrylate or 2-ethylhexyl acrylate, said alkyl acrylate constituting between about 30 percent by weight and about 65 percent by weight of the monomer charge; and

the alkyl methacrylate component (e) is methyl methacrylate, ethyl methacrylate, n-butyl methacrylate, or 2-ethylhexyl methacrylate said vinyl acetate or alkyl methacrylate component (e) constituting be tween about 25 percent by weight and about 60 percent by weight of the monomer charge.

9. A latex paint according to claim 8 wherein:

the alpha, beta-unsaturated carboxylic acid component (a) is methacrylic acid and constitutes between about 0.4 percent by weight and about 1 percent by weight of the monomer charge;

the 'acrylonitrile component (-b) constitutes between about 10 percent by weight and about 12 percent by weight of the monomer charge;

the alpha, beta-unsaturated amide component (0) is N-methylolacrylamide or a hydroxymethyl derivative of diacetone acrylamide and constitutes between about 1.25 percent by weight and about 1.75 percent by weight of the monomer charge; and

the alkyl acrylate component (d) is ethyl acrylate and constitutes between about 40 percent by weight and about 60 percent by weight of the monomer charge; and

component (e) is vinyl acetate and constitutes between about 30 percent by weight and about 50 percent by weight of the monomer charge.

10. A method of coating a surface comprising:

(1) applying to the surface a latex paint comprising a pigmentary material and an aqueous polymer emulsion derived from the interpolymerization. of a monomer charge consisting essentially of:

(a) between about 0.25 percent by weight and about 5 percent by weight based on the total weight of the monomer charge of an alpha, beta-unsaturated carboxylic acid having the following formula:

wherein R is a hydrogen substituent, methyl substituent, or carboxymethyl substituent and R and R are each independently a hydrogen substituent or a carboxy substituent, said carboxylic acid being further characterized in that R and R are not both carboxyl substituents;

(b) greater than 5 percent by weight and less than about 30 percent by weight based on the total weight of the monomer charge of acrylonitrile;

(c) between about 0.5 percent by weight and about 3 percent by weight based on the total weight of the monomer charge of an alpha, beta-unsaturated amide having the following formula:

wherein R is a hydrogen substituent or methyl substituent and R is a hydroxymethyl substituent, an alkoxymethyl substituent wherein the alkyl moiety of said alkoxymethyl substituent contains between 1 and about 8 carbon atoms, or a substituent having the following structure:

CH3 R 0 R5 4-5-11,

Ha a Rs wherein R is a hydrogen substituent or a hydroxymethyl substituent or a hydroxymethyl substituent, with at least one of the R substituents being a hydroxymethyl substituent;

(d) between about 20 percent by weight and about 70 percent by weight based on the total weight of the monomer charge of an alkyl acrylate wherein the alkyl substituent contains between 1 and about 8 carbon atoms; and

(e) between about 20 percent by weight and about 70 percent by weight based on the total weight of the monomer charge of vinyl acetate or an alkyl methacrylate wherein the alkyl substituent contains between 1 and about 8 carbon atoms.

'11. A method according to claim 10 wherein:

the alpha, beta-unsaturated carboxyli acid component (a) is acrylic acid, methacrylic acid, itaconic acid, maleic acid or fumaric acid, said carboxylic acid constituting between about 0.3 percent by weight and about 3 percent by weight of the monomer charge;

the alpha, beta-unsaturated amide component (c) is N- methylolacrylamide, N methoxymethylacrylamide, N-methylolmethacrylamide, N-methoxymethylacrylamide, or a hydroxymethyl derivative of diacetone acrylamide said amide constituting between 1 percent by weight and about 2 percent by weight of the monomer charge;

the alkyl acrylate component (d) is methyl acrylate, ethyl acrylate, n-propyl acrylate, iso-propyl acrylate, n-butyl acrylate or 2-ethylhexyl acrylate, said alkyl acrylate constituting between about 30 percent by weight and about 65 percent by weight of the monomer charge; and

the alkyl methacrylate component (e) is methyl methaerylate, ethyl methacrylate, n-butyl methacrylate or Z-ethylhexyl methacrylate, said vinyl acetate or alkyl methacrylate component (e) constituting between about 25 percent by weight and about 60 percent by Weight of the monomer charge.

12. A method according to claim 11 wherein:

the alpha, beta-unsaturated carboxylic acid component (a) is methacrylic acid and constitutes between about 0.4 percent -by weight and about 1 percent by weight of the monomer charge;

the acrylonitrile component (b) constitutes between about percent by weight and about 12 percent by Weight of the monomer charge;

the alpha, beta-unsaturated amide component (c) is N-methylolacrylamide or a hydroxymethyl derivative of diacetone acrylamide and constitutes between about 1.25 percent by weight and about 1.75 percent by Weight of the monomer charge; and

the alkyl acrylate component (d) is ethyl acrylate and constitutes between about percent by weight and about 60 percent by Weight of the monomer charge; and

component (e) is vinyl acetate and constitutes between about 30 percent by weight and about percent by weight of the monomer charge.

13. An object coated by the composition of claim 1.

References Cited UNITED STATES PATENTS 3,070,561 12/1962 Hager et a1. 26029.6 TA 3,258,443 6/1966 Cantor et a1. 26029.6 TA 3,288,740 11/1966 Maeder et a1. 260-296 TA WILLIAM SHORT, Primary Examiner L. M. PHYNES, Assistant Examiner US. Cl. X.R.

l17l6l UT; 260-17 R, 17.4 ST, 29.6 E, N, Z, 41 B, 78.5 N, BB 

